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The steam temperature is unstable; how should this be addressed in the design?

2017-09-09View Original

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This post was last edited by luckyyjjun on 2017-9-9 at 18:01. Currently, the steam supplied to the client comes from the plant’s heat generation facility; its pressure varies between 8 and 10 atm, while its temperature ranges from 180 to 220°C. This results in significant fluctuations in the existing distillation towers. In the event of a new design, how can these large fluctuations in utility supplies be addressed?
Reply #22017-09-09
The process design selects the heat exchange area based on the poor quality of steam, while the strength design is based on the highest temperature and pressure conditions.
Reply #32017-09-09
But unstable steam can affect the tower pressure, evaporation rate, and stability control; how to address this?
Reply #42017-09-09
Let a control valve regulate the flow rate as a secondary loop, with the flow rate serving as a compensation for temperature and pressure. The bottom of the tower temperature or the sensor plate temperature serves as a secondary circuit for main circuit regulation.
Reply #52017-09-09
The previous set featured a steam buffer tank, with temperature and humidity control, as well as a pressure regulating valve
Reply #62017-09-10
Calculations for the reboiler are considered under low pressure and low temperature conditions, while the system’s design parameters are based on high pressure and high temperature conditions.
Reply #72017-09-10
In fact, it’s not possible for all users to connect directly to the main pipeline without any adjustments; either manual valves or control valves are required. You can solve the problem by installing a pressure control valve or a temperature control valve here.
Reply #82017-09-10
It’s not very large; it has two control valves, one tank, and one pump
Reply #92017-09-10
What the original poster is asking is where to install the pressure control valve or the stability control valve?
Reply #102017-09-11
{:3_68:} There is automatic interlocking between pressure and the valve, so the steam pressure can’t fluctuate suddenly up and down; there is always a certain process involved. An online pressure gauge placed behind the valve will suffice

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